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Waste Heat to Energy Tech Opportunities in US Industry

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Waste Heat to Energy Tech Opportunities in US Industry ( waste-heat-energy-tech-opportunities-us-industry )

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2,500­3,500°F [1,370­1,925°C].84 Exhaust gases are responsible for losses of about 20% of the power input. Half of these losses are due to the chemical energy in the gases, while the other half is sensible heat. Total sensible heat loss via exhaust gases is estimated at about 6 TBtu/yr. Additionally, about 8­10% of energy input is also lost to EAF cooling water “jacket”, totaling an additional 6 TBtu/yr.85 The most common method for heat recovery is scrap preheating, which has been widely used in Europe and Japan for the last thirty years86 and is seeing increased use in the United States. The use of off­gases to preheat scrap can save from 5 to 10% of total EAF energy consumption.87 Initial designs for scrap preheat required piping off­gases to the charging bucket, as shown in Figure 23. Some of the challenges with these systems include the need to transport preheated scrap containing semi­burned non­scrap materials (e.g., plastics), as well the evaporation of volatiles which create odor and environmental control problems.88,89 Alternatives to the bucket preheating system include the Consteel process, the Fuchs shaft furnace, and the Twin shell furnace; retrofit costs range from $4.4 to $6/ton.90 These processes have been installed at various plants in the United States, including Florida Steel, New Jersey Steel, Nucor, North Star, Birmingham Steel, Chapparrel, Gallatin Steel, Steel Dynamics, and Tuscaloosa Steel.91 The Consteel process involves continuous charging of scrap and uses a scrap conveyer, a feeding system, and a preheater. The preheater is a refractory­lined tunnel. Off­gases flow opposite the flow of scrap charge. Air is introduced into the preheater to burn the CO and CO2; consequently both the chemical and sensible heat in the off­gas is used. An afterburner is sometimes installed to burn remaining CO and other compounds.92 The Fuchs shaft furnace involves a shaft immediately above the arc furnace roof. The charge is loaded via baskets in three stages. The baskets are refractory­lined and designed with a seal that prevents the escape of fumes. Scrap heating is further assisted by auxiliary oxy­fuel burners. Additionally, afterburners are installed to completely combust all carbon monoxide. One additional benefit of the system is that charge acts as a dust filter, capturing about 40% of dust and returning it to the furnace, thus enabling slight increases in yield.93 Figure 23 ­ Scrap Preheat System Using a Charging Bucket (source: AISE p. 629) The benefits and drawbacks of scrap preheating systems depend on the specific operation. In some cases, it enables reduced electricity consumption and increased productivity. In other cases, scrap preheating systems are difficult to maintain. As EAFs become increasingly efficient and tap­to­tap times are reduced, scrap handling may reduce productivity and possibly create burdensome maintenance demands. In one case, the energy savings enabled by scrap preheating were reduced by about one half when tap­to­tap times were reduced by a third.94 41 ­

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